diff --git a/docs/source_docs/refs.bib b/docs/source_docs/refs.bib index 899a6d64d461835eecfe9a802705999039bf0d66..98d10e53725a494db5040960ee7c901b52dfec5e 100644 --- a/docs/source_docs/refs.bib +++ b/docs/source_docs/refs.bib @@ -426,6 +426,16 @@ doi = {https://doi.org/10.1016/j.jcp.2022.111305}, doi = {10.1063/1.864230}, } +@article{mehrabadi15, + title={Pseudo-turbulent gas-phase velocity fluctuations in homogeneous gas--solid flow: fixed particle assemblies and freely evolving suspensions}, + author={Mehrabadi, M and Tenneti, S and Garg, R and Subramaniam, S}, + journal={Journal of Fluid Mechanics}, + volume={770}, + pages={210--246}, + year={2015}, + publisher={Cambridge University Press} +} + @article{nijssen20, author = {Tim M.J. Nijssen and Hans A.M. Kuipers and Jan {van der Stel} and Allert T. Adema and Kay A. Buist}, title = {Complete liquid-solid momentum coupling for unresolved CFD-DEM simulations}, @@ -528,7 +538,6 @@ doi = {https://doi.org/10.1016/j.jcp.2022.111305}, publisher={Elsevier} } - @article{suth1893, author = {William Sutherland}, title = {LII. The viscosity of gases and molecular force }, diff --git a/docs/source_docs/user_guide/inputs/fluid_model.rst b/docs/source_docs/user_guide/inputs/fluid_model.rst index 5d71749da0c36759dd2019ac6c790b3e679f3dec..b8ea64ff60113926cbb3d8fe1ef0e19ec99bad69 100644 --- a/docs/source_docs/user_guide/inputs/fluid_model.rst +++ b/docs/source_docs/user_guide/inputs/fluid_model.rst @@ -21,7 +21,9 @@ a single fluid; therefore, it is common to name the fluid ``fluid``. This is ill .. |Reid_4parm_Eq| replace:: :math:`\mu(T) = A\exp{\left( \frac{B}{T} + CT + DT^2 \right)}` -.. |Sato_Eq| replace:: :math:`\mu^* = 1 + C d_s \rho \mu_{mol} \left|\boldsymbol{u} - \boldsymbol{u_s}\right|` +.. |Sato_Eq| replace:: :math:`\mu_{pit} = C d_s \rho \left|\boldsymbol{u} - \boldsymbol{u_s}\right|` + +.. |eff_visc| replace:: :math:`\mu_{eff} = \mu_{mol} + \mu_{eddy} + \mu_{susp} + \mu_{pit}` +--------------------------------------------+------------------------------------------------------------+--------+----------+ | | Description | Type | Default | @@ -110,6 +112,10 @@ a single fluid; therefore, it is common to name the fluid ``fluid``. This is ill | | | | | | | |Sato_Eq| | | | | | | | | +| | * ``Subramaniam`` :cite:p:`mehrabadi15` | | | +| | | | | +| | :math:`\mu_{pit} = C_\mu k_f^2 / \epsilon_f` | | | +| | | | | +--------------------------------------------+------------------------------------------------------------+--------+----------+ | viscosity.suspension.Brinkman.constant | Constant for exponent in Brinkman suspension expression. | Real | None | | | | | | @@ -130,11 +136,14 @@ a single fluid; therefore, it is common to name the fluid ``fluid``. This is ill | viscosity.suspension.Sato.constant | Constant for Sato suspension expression. | Real | 0.65 | | | | | | +--------------------------------------------+------------------------------------------------------------+--------+----------+ +| viscosity.suspension.Subramaniam.constant | Constant for Subramaniam suspension expression. | Real | 0.09 | +| | | | | ++--------------------------------------------+------------------------------------------------------------+--------+----------+ | viscosity.max_effective_factor | Max limit of the effective viscosity as a factor of the | Real | 1.e6 | | | molecular viscosity | | | | | | | | | | :math:`\mu_{eff} < fac*\mu_{mol}`, where | | | -| | :math:`\mu_{eff} = \mu_{mol} + \mu_{eddy} + \mu_{susp}` | | | +| | |eff_visc| | | | +--------------------------------------------+------------------------------------------------------------+--------+----------+ | species | Specify the species that constitute the fluid. | String | None | | | | | |